A combined ultrafiltration-reverse osmosis process for external reuse of Weiyuan shale gas flowback and produced water

被引:55
作者
Guo, Can [1 ,2 ]
Chang, Haiqing [1 ,2 ]
Liu, Baicang [1 ,2 ]
He, Qiping [3 ]
Xiong, Boya [4 ]
Kumar, Manish [4 ]
Zydney, Andrew L. [5 ]
机构
[1] Sichuan Univ, Key Lab Deep Underground Sci & Engn, Minist Educ, Inst New Energy & Low Carbon Technol, Chengdu 610207, Sichuan, Peoples R China
[2] Sichuan Univ, Coll Architecture & Environm, Chengdu 610207, Sichuan, Peoples R China
[3] Chinese Natl Petr Corp, Chuanqing Drilling Engn Co Ltd, Chengdu 610081, Sichuan, Peoples R China
[4] Penn State Univ, Dept Civil & Environm Engn, Greenberg Bldg, University Pk, PA 16802 USA
[5] Penn State Univ, Dept Chem Engn, Greenberg Bldg, University Pk, PA 16802 USA
基金
中国国家自然科学基金; 中国博士后科学基金;
关键词
HYDRAULIC FRACTURING FLOWBACK; WASTE-WATER; MICROFILTRATION MEMBRANES; BARNETT SHALE; DESALINATION; PRESSURE; NANOFILTRATION; REMOVAL; SYSTEMS; PERFORMANCE;
D O I
10.1039/c8ew00036k
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The management of large volumes of flowback and produced water (FPW) generated in shale gas extraction is of great concern due to the high concentrations of total dissolved solids (TDS), scale forming constituents, and organics. The objective of this study was to evaluate the performance of a combined ultrafiltration (UF) and reverse osmosis (RO) process for treating FPW from the Weiyuan shale gas play, China. Under a constant pressure of 4.5 MPa, the RO process decreased the concentrations of TDS, chemical oxygen demand (COD) and Cl-to 192, 7.5 and 97 mg L-1 from 18900, 530 and 11000 mg L-1 in the feed, respectively. The effluent of the combined process met the requirements for surface water discharge and agriculture irrigation in China. The total fouling index of the UF membrane over a range of permeate fluxes suggests a critical flux of around 19 L m-2 h-1; operation at a low flux was effective for UF fouling control. The operating pressure and recovery of the RO system significantly affected the permeate flux and quality, with both the flux and rejection increasing with increasing operating pressure but decreasing with increasing recovery. Moreover, CaCO3 and BaCO3 crystals were identified on the RO membrane surface at high recovery. The rejection data for TDS and COD by the RO membrane were consistent with the SpieglerKedem membrane transport model.
引用
收藏
页码:942 / 955
页数:14
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